US8430803B2 - Method for solidifying and stabilizing waste acid - Google Patents

Method for solidifying and stabilizing waste acid Download PDF

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US8430803B2
US8430803B2 US11/976,341 US97634107A US8430803B2 US 8430803 B2 US8430803 B2 US 8430803B2 US 97634107 A US97634107 A US 97634107A US 8430803 B2 US8430803 B2 US 8430803B2
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waste acid
acid
solidifying
waste
mixed
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Ching-Tsuen Huang
Ching-Tu Chang
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Institute of Nuclear Energy Research
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    • G—PHYSICS
    • G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
    • G21F—PROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
    • G21F9/00—Treating radioactively contaminated material; Decontamination arrangements therefor
    • G21F9/04—Treating liquids
    • G21F9/06—Processing
    • G21F9/16—Processing by fixation in stable solid media
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00—Phosphorus; Compounds thereof
    • C01B25/16—Oxyacids of phosphorus; Salts thereof
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment

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  • This invention relates to a method for treating waste acid, and especially, to a method for solidifying and stabilizing waste acid.
  • the method of the present invention can improve efficiency of the solidifying steps and stability of the solidified waste acid.
  • the radioactive-contaminated metal wastes include stainless steel and carbon steel which use in the construction of the nuclear power plant. Since of the well worn piping of the nuclear power plant has to be replaced, a large amount of the radioactive-contaminated stainless steel should be treated. Decontaminants and methods for decontaminating have been improved and are applied, such as mechanical decontaminating by hydraulic giant; electrochemical decontaminating by a mixture of phosphoric acid, sulfuric acid, and nitric acid; and chemical decontaminating by decontaminant containing fluoroboric acid.
  • the radioactive-contaminated metal wastes can reach regulations on final disposal of low-level waste after treated by the above-mentioned methods.
  • Decontaminant containing phosphoric acid and fluoroboric acid are widely applied in the decontamination of the radioactive metal wastes.
  • the mixture of phosphoric acid and nitric acid is applied for decontaminating of the metal wastes containing copper and aluminum; the mixture of phosphoric acid, sulfuric acid and nitric acid is applied to electrochemical decontaminating suitable for the stainless steel wastes; and the decontaminant containing fluoroboric acid is applied to chemical decontaminating.
  • the metal ions accumulate in the decontaminant gradually. Then, the metal salts precipitated after reached the saturated concentration.
  • the precipitated material in the decontaminant is disadvantageous to the decontaminating process.
  • the treatment of radioactive waste acid still makes progress.
  • the used decontaminant containing fluoroboric acid is treated by destroying the BF 4 ⁇ chelate therein so that CaF 2 can be precipitated.
  • BE 4 which is stable in the room temperature, can be hydrolyzed to form HF by aluminum salt as the catalyst, and then CaF 2 is formed after addition of calcium ion.
  • the aforementioned reactions are the following formulas: 3HBF 4 +Al 2 (SO 4 ) 3 +9H 2 O 2H 3 AlF 6 +3H 3 SO 4 +3H 3 BO 3 ; and H 3 AlF 6 +3Ca(OH) 2 3CaF 2 +Al(OH) 3 +3H 2 O.
  • the amount of aluminum salts has to add more than the concentration of fluoroboric acid so that the efficiency of eliminating fluoroboric acid can be ensured.
  • the conventional method for eliminating fluoroboric acid in waste acid is effective but, however, the amount of the secondary waste will increase.
  • the conventional methods for treating used decontaminant containing phosphoric acid include selectively precipitating and directly neutralizating.
  • the method of selectively precipitating for example, in order to treat 2500 L of used decontaminant containing phosphoric acid, 117 kg of iron powder and 1558.5 kg of oxalic acid is necessary to make phosphoric acid precipitate; 7089 L of water is necessary for solid-liquid separation; and the separated water is needed to neutralize and to eliminate oxalic acid by ultraviolet and ozone. After that, the treated decontaminant has to eliminate the radioactivity further. As described in the U.S. Pat. No.
  • the phosphate ceramic material is applied to treat the solid and liquid wastes.
  • the solid waste is grinded to a size in a range between 4 and 75 micrometers, contacted the grinded powder with phosphate-containing solution to create phosphates of the oxide in a sol-gel, and solidified the sol-gel.
  • the solidified waste is convenient for follow-up treatment.
  • Another object of the present invention is to provide a method for solidifying waste acid by applying at least one solidifying agent to waste acid so that numerous granules in waste acid are formed.
  • the granule is advantageous to reduce the volume of the solidified waste and to improve the mechanical strength thereof.
  • Yet another object of the present invention is to provide a method for solidifying waste acid which can prevent the formation of ettringite.
  • the expansion and chap of the solidified waste caused by ettringite can be prevented and the stabilization thereof can be improved.
  • Still another object of the present invention is to provide a method for solidifying waste acid by adding barium hydroxide to form barium hydrogen phosphate.
  • the formed granule of barium hydrogen phosphate is firm, tiny, solid to coagulate and easy to disperse in waste acid. Waste acid containing granules is easy to flow and to mix with other chemicals.
  • FIG. 1 shows a basic flow diagram of one embodiment of the present invention
  • FIG. 2 shows a basic flow diagram of another embodiment of the present invention.
  • FIG. 3 shows a basic flow diagram of another embodiment of the present invention.
  • a method for solidifying and stabilizing waste acid of the present invention is to improve the efficiency of the solidifying waste acid, to solve the problem of heat generated by the acid-base reaction, and to keep the efficiency of solidification which may be influenced by concentration of waste acid metal ions contained therein.
  • the conventional method for adjusting pH is adding lime (calcium hydroxide) or sodium hydroxide.
  • Calcium phosphate is formed by adding calcium hydroxide in waste acid containing phosphoric acid.
  • low-density ettringite is formed by calcium, which is from calcium phosphate, reacting with tricalcium aluminate in cement.
  • the formed ettringite makes the volume of the solidified product of waste acid expended gradually so that the solidified product becomes chapped.
  • mass of the solidified product should be increased with undesired volume.
  • crystal of phosphoric acid is easy formed in waste acid. Crystal is disadvantageous to deliver solidified waste acid in a duct.
  • granule can be formed so that volume of the solidified waste acid can be reduced and mechanical strength thereof can be improved.
  • FIG. 1 shows a basic flow diagram of one embodiment of the present invention.
  • waste acid containing phosphoric acid can be a mixed waste acid, for example a solution of phosphoric acid and nitric acid, or a solution of nitric acid mixing with phosphoric acid or sulfuric acid.
  • step 100 shown in FIG. 1 condensing waste acid containing waste acid is proceeded by heating and stirring so that water therein is evaporated.
  • step 100 waste acid is condensed in a concentration of 50% to 65% which is suitable for further solidification.
  • a conversion of phosphate is proceeded. Barium hydroxide is added to the condensed waste acid.
  • the condensed waste acid is keeping stirring so that phosphoric acid can react with barium hydroxide to for barium hydrogen phosphate completely.
  • the pH of the mixed waste acid can be adjusted to 2.5-4.5.
  • the preferred pH is 3.
  • a solidifying agents is added so that the waste acid containing barium hydrogen phosphate can be solidified.
  • the solidifying agent should be added to the mixed waste acid in batches or continuously. Temperature of the mixed waste acid during the addition of the solidifying agent should be kept in a range of 30 to 45° C.
  • the preferred way for adding solidifying agents is three times in batches. At first time, a half of total weight of the solidifying agent is added. At the second and the third times, a one-fourth of total weight of the solidifying agent is added, respectively.
  • step S 100 3510 g of waste acid containing phosphoric acid, which the initial concentration of phosphoric acid is 45%, is held in a beaker, heating by a heating plate and stirring by an automatic stirrer so that water in waste acid is vaporized and the weight percent of water in waste acid is reduced.
  • step S 110 the obtained 2700 g of the condensed waste acid is divided into two parts.
  • the applied amount of the solidifying agent is 310 g, and pH of the solidified product produced from waste acid containing phosphoric acid is 3.8.
  • the compression strength of the solidified product which formed after 12 days and after 28 days are 7.8 and 61.2 kg/cm 2 , respectively.
  • the applied amount of solidifying agents is 404.5 g, and pH of the solidified product produced from waste acid containing phosphoric acid is 3.9.
  • the compression strength of the solidified product which formed after 12 days and after 28 days are 101.9 and 112.2 kg/cm 2 , respectively.
  • Table 1 the method for solidifying and stabilizing waste acid of the present invention can make the compression strength of the solidified product steadily on the increase.
  • the additional amounts of the solidifying agent and the neutralizer make a better characteristic of the solidified product of waste acid.
  • waste acid containing phosphoric acid before condensing is 1755 g and total volume thereof is 1013.3 ml.
  • waste acid is solidified to form a solidified product.
  • the total weight and volume of the solidified product is 1572.5 g and 834 ml, respectively.
  • the weight and volume of waste acid can be reduced by the method for solidifying and stabilizing waste acid of the present invention.
  • FIG. 2 shows a basic flow diagram of another embodiment of the present invention.
  • the difference between FIG. 1 and FIG. 2 is that in the steps of FIG. 1 , barium hydroxide and the solidifying agent are added to solidify waste acid, but in the steps of FIG. 2 , barium hydroxide is added to waste acid containing fluoroboric acid and then mixed with waste acid containing phosphoric acid to form a mixed waste acid.
  • a granule is formed by adding a first solidifying agent to the mixed waste acid, and a solidified product of the mixed waste acid is formed by adding a second solidifying agent.
  • waste acid containing phosphoric acid is condensed to a concentration of 55%.
  • step of S 210 barium hydroxide is added to waste acid containing fluoroboric acid to form a precipitation of barium fluoride (BaF 2 ), and then, is mixed with the condensed waste acid containing phosphoric acid in the concentration of 55% to form a stable mixed waste acid.
  • the weight ratio of waste acid containing phosphoric acid to waste acid containing fluoroboric acid is six.
  • the mixed waste acid is added by dropping to a first solidifying agent so that a plurality of small granule in the mixed waste acid are formed.
  • the first solidifying agent is consisted of cement, slag, and fly ash.
  • the formed granule is added to another half of the mixed waste acid which is kept stirring.
  • a second solidifying agent is added to another half of the mixed waste acid to solidify. Since the granule in the mixed waste acid is as an aggregate in the solidified product. Weight of the formed solidified product can be reduced.
  • the second solidifying agent is cement.
  • step of S 200 6282 g of waste acid containing phosphoric acid is condensed to 5140 g with a concentration of 55%.
  • step of S 210 barium hydroxide is added to waste acid containing fluoroboric acid, and then is mixed with the condensed waste acid containing phosphoric acid to form a mixed waste acid.
  • weight of waste acid containing fluoroboric acid is 860 g
  • applied amount of barium hydroxide is 396 g.
  • step of S 220 3029 g of the solidifying agent is mixed with the mixed waste acid to form the granules.
  • the weight of waste acid containing phosphoric acid before condensing is 1571 g
  • total weight of waste acid containing fluoroboric acid is 215 g
  • the weight ratio of the applied amount of the total solidifying agent to the mixed waste acid is 30.1%.
  • the compression strength of the solidified product which formed after 3 days and after 28 days are 25 kg and 28 kg/cm 2 , respectively.
  • the result of compression strength after dipping in water for three months is 53.5 kg/cm 2 .
  • the solidified product of waste acid formed by the method of the invention has improved weather resistance and water resistance characteristics.
  • Table 4 the granule is formed by the first solidifying agent and the efficiency of solidification would not be influenced.
  • a half of waste acid is inactivated, and then another half of waste acid is combined therewith to solidify. Heat of acid-base reaction and rapid setting caused by heat can be prevented to influence the quality of the solidified product of waste acid so that the compression strength of the solidified product can be improved.
  • FIG. 3 shows a basic flow diagram of another embodiment of the present invention.
  • barium hydroxide is added to waste acid containing fluoroboric acid, and mixed with waste acid containing phosphoric acid to form a mixed waste acid.
  • the difference is that waste acid containing fluoroboric acid is mixed with waste acid containing phosphoric acid to form a mixed waste acid, and then added barium hydroxide to the mixed waste acid.
  • the waste acid containing phosphoric acid is condensed to a concentration in a range of 50% to 65%.
  • the condensed waste acid which the concentration is from 50% to 65%, is mixed with waste aid containing fluoroboric acid to form a mixed waste acid.
  • the weight ratio of waste acid containing phosphoric acid to waste containing fluoroboric acid is six.
  • barium hydroxide is added to the mixed waste acid to adjust the pH of the mixed waste acid.
  • the mixed waste acid is held by stirring for one hour so that barium hydroxide can completely react with phosphoric acid and fluoroboric acid in the mixed waste acid which pH is 2.5 to 4.5.
  • a solidifying agent is added in bathes when the mixed waste acid is stirring.
  • the preferred way for adding the solidifying agent is three times in batches. At first time, a half of total weight of the solidifying agent is added. At the second and the third times, a one-fourth of total weight of the solidifying agent is added, respectively.
  • the solidifying agent is consisted of cement, slag, silicon ash, and fly ash. Temperature of the mixed waste acid during the addition of the solidifying agent should be kept in a range of 30 to 45° C.
  • step of S 300 5711 g of waste acid containing phosphoric acid, which indicated as No. B5, is condensed by heating and stirring.
  • the condensed waste acid is 5140 g.
  • step of S 310 the condensed waste acid is mixed with 860 g of waste acid containing fluoroboric acid to form a mixed waste acid.
  • step of S 320 840 g of barium hydroxide is added to the mixed waste acid.
  • the mixed waste acid is held for one hour so that the added barium hydroxide can completely react with the mixed waste acid.
  • a solidifying agent is added to the mixed waste acid in batches.
  • the solidifying agent which the total weight is 1560 g, includes 1200 g of cement, 96 g of slag, 172 g of silicon ash, and 504 g of fly ash.
  • the weight ratio of the applied solidifying agent to the mixed waste acid is 23.74%, and the weight ratio of the solidifying agent with a neutralizer to the mixed waste acid is 36.83%.
  • the compression strength of the solidified product formed after 28 days is 27.0 kg/cm 2 .
  • the compression strength of the solidified product after dipped three months is 60 kg/cm 2 .

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Abstract

The present invention discloses a method for solidifying and stabilizing waste acid including steps of condensing waste acid containing phosphoric acid to reduce the volume; mixing the condensed waste acid with waste acid containing fluoroboric acid to solidify and stabilize the mixed waste acid. The pH of the mixed acid is adjusted by adding barium hydroxide as a neutralizer. The efficiency of solidifying waste acid can be improved by partially granulating and by adding solidifying agent indirectly. The method of the present invention can prevent intensely exothermic reaction caused by adding solidifying agents. Furthermore, the method of the present invention is controlled in a temperature of 30 to 45° C. to improve the polymerization of the mixed waste acid so that the efficiency of solidification thereof can be also improved.

Description

BACKGROUND OF THE INVENTION
1. Field of Invention
This invention relates to a method for treating waste acid, and especially, to a method for solidifying and stabilizing waste acid. The method of the present invention can improve efficiency of the solidifying steps and stability of the solidified waste acid.
2. Related Art
In general, the radioactive-contaminated metal wastes include stainless steel and carbon steel which use in the construction of the nuclear power plant. Since of the well worn piping of the nuclear power plant has to be replaced, a large amount of the radioactive-contaminated stainless steel should be treated. Decontaminants and methods for decontaminating have been improved and are applied, such as mechanical decontaminating by hydraulic giant; electrochemical decontaminating by a mixture of phosphoric acid, sulfuric acid, and nitric acid; and chemical decontaminating by decontaminant containing fluoroboric acid. The radioactive-contaminated metal wastes can reach regulations on final disposal of low-level waste after treated by the above-mentioned methods.
Decontaminant containing phosphoric acid and fluoroboric acid are widely applied in the decontamination of the radioactive metal wastes. For example, the mixture of phosphoric acid and nitric acid is applied for decontaminating of the metal wastes containing copper and aluminum; the mixture of phosphoric acid, sulfuric acid and nitric acid is applied to electrochemical decontaminating suitable for the stainless steel wastes; and the decontaminant containing fluoroboric acid is applied to chemical decontaminating. During the decontaminating process, the metal ions accumulate in the decontaminant gradually. Then, the metal salts precipitated after reached the saturated concentration. The precipitated material in the decontaminant is disadvantageous to the decontaminating process. Moreover, if the decontaminant is contaminated by the nuclides and the radioactivity thereof raises, the decontaminant should be regenerated. Metal ions of the recycled decontaminant containing phosphoric acid and fluoroboric acid can be removed by way of oxalic acid selective precipitation, electrolysis recovery, and cation exchange, so that the decontaminant can be recovered and reused thereafter. After several times of the regenesis, decontaminant has to be eliminated since the radioactivity thereof is high. The used decontaminant becomes waste acid.
At the present day, the treatment of radioactive waste acid still makes progress. In the conventional process, the used decontaminant containing fluoroboric acid is treated by destroying the BF4 − chelate therein so that CaF2 can be precipitated. BE4, which is stable in the room temperature, can be hydrolyzed to form HF by aluminum salt as the catalyst, and then CaF2 is formed after addition of calcium ion. The aforementioned reactions are the following formulas:
3HBF4+Al2(SO4)3+9H2O
Figure US08430803-20130430-P00001
2H3AlF6+3H3SO4+3H3BO3; and
H3AlF6+3Ca(OH)2
Figure US08430803-20130430-P00001
3CaF2+Al(OH)3+3H2O.
In the formulas, the amount of aluminum salts has to add more than the concentration of fluoroboric acid so that the efficiency of eliminating fluoroboric acid can be ensured. The conventional method for eliminating fluoroboric acid in waste acid is effective but, however, the amount of the secondary waste will increase.
The conventional methods for treating used decontaminant containing phosphoric acid include selectively precipitating and directly neutralizating. In the method of selectively precipitating, for example, in order to treat 2500 L of used decontaminant containing phosphoric acid, 117 kg of iron powder and 1558.5 kg of oxalic acid is necessary to make phosphoric acid precipitate; 7089 L of water is necessary for solid-liquid separation; and the separated water is needed to neutralize and to eliminate oxalic acid by ultraviolet and ozone. After that, the treated decontaminant has to eliminate the radioactivity further. As described in the U.S. Pat. No. 5,645,518 which is titled “Method for stabilizing low-level mixed wastes at room temperature”, the phosphate ceramic material is applied to treat the solid and liquid wastes. The solid waste is grinded to a size in a range between 4 and 75 micrometers, contacted the grinded powder with phosphate-containing solution to create phosphates of the oxide in a sol-gel, and solidified the sol-gel. The solidified waste is convenient for follow-up treatment.
As described above, the conventional methods for treating waste acid have disadvantages including: (1) a large amount of the neutralizer is necessary to mix with the same amount of waste acid so that the effect of compaction of waste acid is undesired; (2) the solid sludge and liquid waste generated during treating of waste acid have to treat by another process so that the secondary contamination and the large amount of waste are undesired; (3) heat generated during the treatment of waste acid is hard to control so that the rapid setting caused by heat is disadvantageous to waste acid; and (4) applying neutralizers separately to waste acid is adverse for stabilization of waste acid. The aforementioned disadvantages should be eliminated to improve the solidification and stabilization of waste acid.
In this regard, it is important to provide a method for solidifying and stabilizing waste acid which prevents formation of secondary contamination, has low cost, simplify the processes, and improves the efficiency of solidification to eliminate the foregoing drawbacks.
SUMMARY OF THE INVENTION
Accordingly, it is an object of the present invention to provide a method for treating waste acid to solidify and stabilize by adding barium hydroxide to adjust the pH of waste acid so that waste acid can be stabilized and the corrosion thereof can be reduced.
Another object of the present invention is to provide a method for solidifying waste acid by applying at least one solidifying agent to waste acid so that numerous granules in waste acid are formed. The granule is advantageous to reduce the volume of the solidified waste and to improve the mechanical strength thereof.
Yet another object of the present invention is to provide a method for solidifying waste acid which can prevent the formation of ettringite. The expansion and chap of the solidified waste caused by ettringite can be prevented and the stabilization thereof can be improved.
Still another object of the present invention is to provide a method for solidifying waste acid by adding barium hydroxide to form barium hydrogen phosphate. The formed granule of barium hydrogen phosphate is firm, tiny, solid to coagulate and easy to disperse in waste acid. Waste acid containing granules is easy to flow and to mix with other chemicals.
In order to achieve the above objects, the present invention provides a method for solidifying and stabilizing waste acid including the steps of condensing waste acid containing phosphoric acid; adding barium hydroxide to the condensed waste acid and adjusting the pH thereof to form barium hydrogen phosphate; and adding solidifying agents to solidify barium hydrogen phosphate. In the step of adding barium hydroxide is for adjusting the pH of waste acid and for stabilizing waste acid. The adjusted pH of waste acid can improve the formation of barium hydrogen phosphate. In the step of adding the solidifying agents is adding in batches or continuously so that heat, which generated by the intense reaction and is disadvantageous to solidification, can be prevented. In the method of present invention, waste acid containing phosphoric acid can form granule by adding solidifying agents to reduce the volume of waste acid. Moreover, waste acid containing phosphoric acid can mix with another waste acid containing fluoroboric acid. The pH of the mixed waste acid can be adjusted by adding barium hydroxide so that the stability of the mixed waste acid can be kept. The concentration of the solution and metal ion will not obstruct the solidifying reaction of the mixed waste acid.
BRIEF DESCRIPTION OF THE DRAWINGS
The invention can be more fully understood by reading the subsequent detailed description and examples with references made to the accompanying drawings, wherein:
FIG. 1 shows a basic flow diagram of one embodiment of the present invention;
FIG. 2 shows a basic flow diagram of another embodiment of the present invention; and
FIG. 3 shows a basic flow diagram of another embodiment of the present invention.
 DETAILED DESCRIPTION OF THE INVENTION
A method for solidifying and stabilizing waste acid of the present invention is to improve the efficiency of the solidifying waste acid, to solve the problem of heat generated by the acid-base reaction, and to keep the efficiency of solidification which may be influenced by concentration of waste acid metal ions contained therein. The conventional method for adjusting pH is adding lime (calcium hydroxide) or sodium hydroxide. Calcium phosphate is formed by adding calcium hydroxide in waste acid containing phosphoric acid. However, during the solidifying reaction of waste acid, low-density ettringite is formed by calcium, which is from calcium phosphate, reacting with tricalcium aluminate in cement. The formed ettringite makes the volume of the solidified product of waste acid expended gradually so that the solidified product becomes chapped. In order to eliminate expansion and chap of the solidified product of waste acid, mass of the solidified product should be increased with undesired volume. Besides, crystal of phosphoric acid is easy formed in waste acid. Crystal is disadvantageous to deliver solidified waste acid in a duct. During the solidifying step of the present invention, granule can be formed so that volume of the solidified waste acid can be reduced and mechanical strength thereof can be improved. The present invention will be apparent from the following detailed description, which proceeds with reference to the accompanying drawings.
FIG. 1 shows a basic flow diagram of one embodiment of the present invention. In the embodiment, waste acid containing phosphoric acid can be a mixed waste acid, for example a solution of phosphoric acid and nitric acid, or a solution of nitric acid mixing with phosphoric acid or sulfuric acid. As the step 100 shown in FIG. 1, condensing waste acid containing waste acid is proceeded by heating and stirring so that water therein is evaporated. After step 100, waste acid is condensed in a concentration of 50% to 65% which is suitable for further solidification. Next, in the step S110, a conversion of phosphate is proceeded. Barium hydroxide is added to the condensed waste acid. During the addition of barium hydroxide, the condensed waste acid is keeping stirring so that phosphoric acid can react with barium hydroxide to for barium hydrogen phosphate completely. Furthermore, the pH of the mixed waste acid can be adjusted to 2.5-4.5. In the embodiment, the preferred pH is 3. In step 120, when pH of the mixed waste acid is in a range of 2.5 to 4.5, a solidifying agents is added so that the waste acid containing barium hydrogen phosphate can be solidified. The solidifying agent should be added to the mixed waste acid in batches or continuously. Temperature of the mixed waste acid during the addition of the solidifying agent should be kept in a range of 30 to 45° C. In the embodiment, the preferred way for adding solidifying agents is three times in batches. At first time, a half of total weight of the solidifying agent is added. At the second and the third times, a one-fourth of total weight of the solidifying agent is added, respectively.
The following is a detailed description of the embodiment shown in FIG. 1. In the step S100, 3510 g of waste acid containing phosphoric acid, which the initial concentration of phosphoric acid is 45%, is held in a beaker, heating by a heating plate and stirring by an automatic stirrer so that water in waste acid is vaporized and the weight percent of water in waste acid is reduced. After the heating step, 2700 g of the condensed waste acid is obtained and the concentration of phosphoric acid in the condensed waste acid is in a range between 50% and 65%. In the step of S110, the obtained 2700 g of the condensed waste acid is divided into two parts. Two parts of 1350 g of the condensed waste acid are held in two mixers, and 189 g and 181.6 g of barium hydroxide are added to the mixers, respectively. The mixer is kept running for one hour so that phosphoric acid in the condensed waste acid is converted to generate barium hydrogen hydroxide. In this step, barium hydroxide is for adjusting pH of the condensed waste acid and for stabilizing thereof. After addition of barium hydroxide, barium hydrogen hydroxide is generated and pH of the condensed waste acid raises to 3.
As mentioned before, in the result of adding 181.6 g of monohydrous barium hydroxide which is as a neutralizer, the applied amount of the solidifying agent is 310 g, and pH of the solidified product produced from waste acid containing phosphoric acid is 3.8. The compression strength of the solidified product which formed after 12 days and after 28 days are 7.8 and 61.2 kg/cm2, respectively. Besides, in the result of adding 189 g of monohydrous barium hydroxide which is as a neutralizer, the applied amount of solidifying agents is 404.5 g, and pH of the solidified product produced from waste acid containing phosphoric acid is 3.9. The compression strength of the solidified product which formed after 12 days and after 28 days are 101.9 and 112.2 kg/cm2, respectively. As shown in Table 1 below, the method for solidifying and stabilizing waste acid of the present invention can make the compression strength of the solidified product steadily on the increase. The additional amounts of the solidifying agent and the neutralizer make a better characteristic of the solidified product of waste acid.
TABLE 1
Results of solidification of waste acid containing phosphoric acid
Conditions Result of solidification
Applied amount of Applied amount pH of the Compression Compression
the neutralizer Total weight Total weight of the solidified strength after strength after
(monohydrous before after solidifying product of 12 days 28 days
barium hydroxide) (g) condensing (g) condensing (g) agent (g) waste acid (kg/cm2) (kg/cm2)
181.6 1755 1350 310.0 3.8 7.8 61.2
189 1755 1350 404.5 3.9 101.9 112.2
Assuming that the total weight of waste acid containing phosphoric acid before condensing is 1755 g and total volume thereof is 1013.3 ml. After adding barium hydroxide, and adding the solidifying agent in batches, waste acid is solidified to form a solidified product. The total weight and volume of the solidified product is 1572.5 g and 834 ml, respectively. As shown in Table 2 below, the weight and volume of waste acid can be reduced by the method for solidifying and stabilizing waste acid of the present invention.
TABLE 2
Results of solidification of waste acid containing phosphoric acid
Conditions
Total weight Total weight Volume of Result of solidification
of waste acid of waste acid waste acid Specific Weight ratio Volume ratio
before after before Weight of the Volume of the gravity of the of IER/ of IER/
condensing condensing condensing solidifying solidifying solidifying solidifying solidifying
(g) (g) (ml) agent (g) agent (ml) agent agent agent
1755 1350 1013.3 1572.5 834 1.88 1.116 1.215
FIG. 2 shows a basic flow diagram of another embodiment of the present invention. The difference between FIG. 1 and FIG. 2 is that in the steps of FIG. 1, barium hydroxide and the solidifying agent are added to solidify waste acid, but in the steps of FIG. 2, barium hydroxide is added to waste acid containing fluoroboric acid and then mixed with waste acid containing phosphoric acid to form a mixed waste acid. A granule is formed by adding a first solidifying agent to the mixed waste acid, and a solidified product of the mixed waste acid is formed by adding a second solidifying agent. In the step of S200 shown in FIG. 2, waste acid containing phosphoric acid is condensed to a concentration of 55%. In the step of S210, barium hydroxide is added to waste acid containing fluoroboric acid to form a precipitation of barium fluoride (BaF2), and then, is mixed with the condensed waste acid containing phosphoric acid in the concentration of 55% to form a stable mixed waste acid. In the mixed waste acid, the weight ratio of waste acid containing phosphoric acid to waste acid containing fluoroboric acid is six. In the step 220, the mixed waste acid is added by dropping to a first solidifying agent so that a plurality of small granule in the mixed waste acid are formed. The first solidifying agent is consisted of cement, slag, and fly ash. In the step of S230, the formed granule is added to another half of the mixed waste acid which is kept stirring. Next, a second solidifying agent is added to another half of the mixed waste acid to solidify. Since the granule in the mixed waste acid is as an aggregate in the solidified product. Weight of the formed solidified product can be reduced. In the embodiment, the second solidifying agent is cement.
The following is a detailed description of the embodiment shown in FIG. 2. In the step of S200, 6282 g of waste acid containing phosphoric acid is condensed to 5140 g with a concentration of 55%. In the step of S210, barium hydroxide is added to waste acid containing fluoroboric acid, and then is mixed with the condensed waste acid containing phosphoric acid to form a mixed waste acid. In the embodiment, weight of waste acid containing fluoroboric acid is 860 g, and applied amount of barium hydroxide is 396 g. In the step of S220, 3029 g of the solidifying agent is mixed with the mixed waste acid to form the granules. After the granulating, weight of liquid in the mixed waste acid reduced to 68.91% in comparison with the mixed waste acid before granulating. In contrast, the steps shown in FIG. 2 are carried out by 6747 g of waste acid containing phosphoric acid with a concentration of 50%, 1122 g of waste acid containing fluoroboric acid, 524 g of barium hydroxide, and 4223 g of the first solidifying agent. After the granulating, weight of liquid in the mixed acid reduced to 77.72% in comparison with the mixed waste acid before granulating. The foregoing results are listed in the Table 3. The weight of liquid in waste acid can be reduced by the method for solidifying and stabilizing waste acid of the invention.
TABLE 3
Results of granulation of waste acid containing phosphoric acid mixed with fluoroboric acid
Conditions Results of granulation
Total weight Total weight Total weight of
Concentration of of waste acid of waste acid the granule after
waste acid containing containing Total weight Applied amount Applied Total weight granulation/
containing phosphoric phosphoric of waste acid of the neutralizer amount of the mixted waste
phosphoric acid acid before acid after containing (monohydrous of the granule acid + Applied
after condensed condensing condensed fluoroboric barium solidifying after amount of the
(%) (g) (g) acid (g) hydroxide) (g) agent granulation neutralizer
55 6282 5140 860 396 3029 7282.2 68.91
50 7500 6747 1122 524 4223 10391 77.72
In the step of S230, the weight of waste acid containing phosphoric acid before condensing is 1571 g, total weight of waste acid containing fluoroboric acid is 215 g applied amount of barium hydroxide is 210 g, and the weight ratio of the applied amount of the total solidifying agent to the mixed waste acid is 30.1%. After solidifying, the compression strength of the solidified product which formed after 3 days and after 28 days are 25 kg and 28 kg/cm2, respectively. Furthermore, in the water-resistance test of the sample which the compression strength is 74 kg per square centimeter, the result of compression strength after dipping in water for three months is 53.5 kg/cm2. It indicated that the solidified product of waste acid formed by the method of the invention has improved weather resistance and water resistance characteristics. As shown in Table 4, the granule is formed by the first solidifying agent and the efficiency of solidification would not be influenced. In the steps shown in FIG. 2, a half of waste acid is inactivated, and then another half of waste acid is combined therewith to solidify. Heat of acid-base reaction and rapid setting caused by heat can be prevented to influence the quality of the solidified product of waste acid so that the compression strength of the solidified product can be improved.
TABLE 4
Results of solidification and granulation of waste acid containing phosphoric acid mixed with fluoroboric acid
Conditions
Mixed waste acid Results of solidification
Weight of Total weight Total weight Applied amount Applied Compression
granule after of phosphoric of waste acid of neutralizer Applied amount of Compression strength strength
partially acid before containing (monohydrous amount solidifying (kg/cm2 after dipping
granulation condensing fluoroboric barium of cement agent/Mixed After After After 3 months
(g) (g) acid (g) hydroxide) (g) (g) waste acid (%) 3 days 14 days 28 days (kg/cm2)
1875 1571 215 210 — 30.1 25 28
1875 1393 189 210 — 31.9 35 51
1657 1231 167 186 — 30.1 21 29
Results of dipping the solidified product
5195 3750 561 262.2 340 34.1 67.5 78.5 74 53.5
4097 2810 423 197 318 31.6 33 52 64 42.5
4097 2810 423 197 283.3 31.2 33.5 48 45 38.3
FIG. 3 shows a basic flow diagram of another embodiment of the present invention. In the steps of FIG. 2, barium hydroxide is added to waste acid containing fluoroboric acid, and mixed with waste acid containing phosphoric acid to form a mixed waste acid. In the steps of FIG. 3, the difference is that waste acid containing fluoroboric acid is mixed with waste acid containing phosphoric acid to form a mixed waste acid, and then added barium hydroxide to the mixed waste acid. In the step of S300, the waste acid containing phosphoric acid is condensed to a concentration in a range of 50% to 65%. In the step of S310, the condensed waste acid, which the concentration is from 50% to 65%, is mixed with waste aid containing fluoroboric acid to form a mixed waste acid. In the mixed waste acid, the weight ratio of waste acid containing phosphoric acid to waste containing fluoroboric acid is six. In the step of S320, barium hydroxide is added to the mixed waste acid to adjust the pH of the mixed waste acid. Next, the mixed waste acid is held by stirring for one hour so that barium hydroxide can completely react with phosphoric acid and fluoroboric acid in the mixed waste acid which pH is 2.5 to 4.5. In step of S330, a solidifying agent is added in bathes when the mixed waste acid is stirring. In the embodiment, the preferred way for adding the solidifying agent is three times in batches. At first time, a half of total weight of the solidifying agent is added. At the second and the third times, a one-fourth of total weight of the solidifying agent is added, respectively. The solidifying agent is consisted of cement, slag, silicon ash, and fly ash. Temperature of the mixed waste acid during the addition of the solidifying agent should be kept in a range of 30 to 45° C.
The following is a detailed description of the embodiment shown in FIG. 3. In the step of S300, 5711 g of waste acid containing phosphoric acid, which indicated as No. B5, is condensed by heating and stirring. The condensed waste acid is 5140 g. In the step of S310, the condensed waste acid is mixed with 860 g of waste acid containing fluoroboric acid to form a mixed waste acid. In the step of S320, 840 g of barium hydroxide is added to the mixed waste acid. The mixed waste acid is held for one hour so that the added barium hydroxide can completely react with the mixed waste acid. Next, in the step of S30, a solidifying agent is added to the mixed waste acid in batches. The solidifying agent, which the total weight is 1560 g, includes 1200 g of cement, 96 g of slag, 172 g of silicon ash, and 504 g of fly ash. The weight ratio of the applied solidifying agent to the mixed waste acid is 23.74%, and the weight ratio of the solidifying agent with a neutralizer to the mixed waste acid is 36.83%. The compression strength of the solidified product formed after 28 days is 27.0 kg/cm2. The compression strength of the solidified product after dipped three months is 60 kg/cm2.
The result of foregoing steps is shown in Table 5. Besides, two results which indicated as Nos. B6 and B7 shown in Table 5 are similar to the result of No. B5. As the results shown in Table 5 indicated, the solidified product of waste acid formed by the method of the invention has improved weather resistance and water resistance characteristics. Moreover, the method of the invention prevents intensely exothermic reaction and rapid setting caused by adding the solidifying agents to influence the efficiency and quality of solidification.
TABLE 5
Results of indirect solidification of waste acid containing phosphoric acid mixed with fluoroboric acid
Conditions
Total weight Total weight Results
of waste acid of waste acid Applied Applied amount Applied amount
containing containing Total weight amount of of solidifying of solidifying Compression
phosphoric phosphoric of waste acid neutralizer Applied agent/Total agent + Compression strength
acid before acid after containing (monohydrous amount of weight of mixed neutralizer/Total strength after dipping
condensing condensed fluoroboric barium solidifying waste acid weight of mixed after 28 days 3 months
No. (g) (g) acid (g) hydroxide) (g) agent (%) (%) waste acid (%) (kg/cm2) (kg/cm2)
B5 5711 5140 860 840 1560 23.74 36.83 27.0 60
B6 5711 5140 860 640 1560 23.74 33.48 16.0 43
B7 5711 5140 860 840 1705 25.95 39.73 48.5 103
While the invention is susceptible to various modifications and alternative forms, specific embodiments thereof have been shown by the way of example in the drawings and are herein described in detail. It should be understood, however, that the description herein of specific embodiments is not intended to limit the invention to the particular forms disclosed, but on the contrary, the intention is to cover all modifications, equivalents, and alternatives falling within the spirit and scope of the invention ad defined by the appended claims.

Claims (4)

We claim:
1. A method for solidifying and stabilizing waste acid comprising steps of:
condensing the waste acid containing phosphoric acid to obtain a higher concentration condensed waste acid
adding barium hydroxide to the condensed waste acid and adjusting the pH of the condensed waste acid to an acidic pH, thereby generating barium hydrogen phosphate; and
adding a solidifying agent to react with the barium hydrogen phosphate to form a solidified product of the condensed waste acid.
2. The method as recited in claim 1, wherein the step of adding the solidifying agent is adding in batches or continuously so that the condensed waste acid can be controlled in a temperature of 30 to 45° C.
3. The method as recited in claim 1, wherein adjusting the pH of the condensed waste acid is adjusting the pH to a range between 2.5 and 4.5.
4. The method as recited in claim 1, wherein condensing the waste acid is condensing to a concentration of at least 50% of phosphoric acid.
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US4652381A (en) * 1985-07-22 1987-03-24 Farmland Industries, Inc. Battery plant waste water treatment process
US5645518A (en) 1995-01-31 1997-07-08 The University Of Chicago Method for stabilizing low-level mixed wastes at room temperature
JPH09253658A (en) * 1996-03-27 1997-09-30 Kurita Water Ind Ltd Method for treating waste water containing concentrated phosphoric acid
US6133498A (en) * 1999-05-05 2000-10-17 The United States Of America As Represented By The United States Department Of Energy Method for producing chemically bonded phosphate ceramics and for stabilizing contaminants encapsulated therein utilizing reducing agents
US6204214B1 (en) * 1996-03-18 2001-03-20 University Of Chicago Pumpable/injectable phosphate-bonded ceramics

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4652381A (en) * 1985-07-22 1987-03-24 Farmland Industries, Inc. Battery plant waste water treatment process
US5645518A (en) 1995-01-31 1997-07-08 The University Of Chicago Method for stabilizing low-level mixed wastes at room temperature
US6204214B1 (en) * 1996-03-18 2001-03-20 University Of Chicago Pumpable/injectable phosphate-bonded ceramics
JPH09253658A (en) * 1996-03-27 1997-09-30 Kurita Water Ind Ltd Method for treating waste water containing concentrated phosphoric acid
US6133498A (en) * 1999-05-05 2000-10-17 The United States Of America As Represented By The United States Department Of Energy Method for producing chemically bonded phosphate ceramics and for stabilizing contaminants encapsulated therein utilizing reducing agents

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